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Synthesis and Characterization of Niobium Carbide with Copper Addition Obtained Via

Gas Solid Reaction

Maria Veronilda Macedo Soutoa* , Camila Pacelly Brandão de Araujob, Maria José Santos Limaa,

Filipe Martel Magalhães Borgesc , Uilame Umbelino Gomesa, Carlson Pereira de Souzab

Received: December 20, 2016; Revised: October 17, 2017; Accepted: January 18, 2018

The use of niobium containing materials' has gained much attention of the scientific community in the late years due its various applications in diverse fields. NbC is a highly versatile material. Copper addition may alter several of its properties, such as morphology, crystal structure etc. as well as enhance its catalytic behavior. Nanostructured NbC with copper addition synthesis' presented here had the precursor [(NH4)3[NbO(C2O4)3]xH2O] as starting material, which was doped with Cu(NO3)2 at 5% and 10% (molar) ratios. Doped NbC was obtained via gas solid reaction in fixed bed reactor at lower temperature (980°C) and with shorter reaction time (2h) than traditional methods. Reaction products' were characterized by XRD, crystal sizes were estimated according to HWL method, and SEM, XRF, BET and laser particle size analysis were performed. XRD indicated the formation of NbC and Cu phases with cubic crystal structure of ~20nm. SEM showed slight morphological change upon increasing copper content, indicating a less porous structure, which is consistent with BET data (43.7m2/g for 5%Cu-NbC and 37m 2/g for the 10% Cu-NbC). Crystal size calculations showed that increasing dopant content particle sizes were also increased, probably due to the presence of the dopant, in some extent, in the crystal structure.

Keywords: Niobium carbide, copper, gas solid reaction, fixed bed reactor.

*e-mail Veronilda.macedo@gmail.com

1. Introduction

Recently, the development of materials with various

applications has become a major industrial interest; in that sense, researches have been developed considering and thus aiming to change synthesis conditions or parameters, so

that time and energy requirements can be minimized and, ideally, more versatile materials can be obtained. Refractory

metals' carbides are highly versatile materials as their

range of proprieties is wide: extreme hardness, resistance

to degas, excellent resistance to high temperature (high

melting point), etc.1,2.

Industrial production of these materials, however, is

only possible through highly energetic processes at elevated

temperatures (>1300°C)5 for long residence times (over 6h)6, which makes the production of nanoscale products difficult7. The development of reaction routes that apply lower temperatures and reaction times, such as the one presented in this paper, could be more interesting economically and industrially, not to mention the gains in materials' properties

(nanoscale products, higher superficial area, etc.).

Among refractory carbides, niobium carbide has received

much attention of the scientific community due to its valuable

set of proprieties, among which its extreme hardness [>235GPa] is worth notice3,4. Besides, niobium materials are a topic of interest as Brazil holds the majority of its minerals' reserves and the development of fully finished products is important in a strategically point of view.

Niobium carbide is a highly versatile material as it has

applications on the metallurgy industry, aerospace industry,

and others, as well as on the catalytic field. Especially for hydrodesulphurization reactions of oil refining industries

for environmental compliance, carbide catalysts have been found to be excellent reacting materials9,10. For its use as catalysts, carbides are required to present high surface

areas, small particle sizes, as well as a surface free from

pollutants, such as free carbon, that can impair the catalytic reaction11,12. Niobium based catalysts are effective in different processes, such as hydrogenation, oxidation, esterification, polymerization, and condensation reactions13.

Usually, in those catalytic reactions a promoting metal is used14. Often enough these metals are com Ni+2, Co+2, Cu+. Souza et al.15 produced chromium-copper composites and upon evaluating the synergistic effect of those metals, concluded that the addition of Cu caused structural modification of the

original catalysts and activated catalytic sites, thus increasing

its activity. Samir et al.16 also used a copper composite in

aDepartamento de Ciência e Engenharia de Materiais, Universidade Federal do Rio Grande do Norte,

Natal, RN, Brasil

bLaboratório de Materiais Nanoestruturados e Reatores Catalíticos, Departamento de Engenharia

Química, Universidade Federal do Rio Grande do Norte, Natal, RN, Brasil

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organic catalytic reactions and owed to copper addition the catalytic gain observed.

For the synthesis of niobium carbide with the copper addition high energy milling followed by sintering is the traditional route. In this process metallic copper and graphite

are used as starting materials17,18,19. This methodology, however,

leads to powders with larger particle sizes and require long processing times. The TPR method (temperature programmed reaction) is an alternative to produce these materials with high particle size control due to the increased interaction between gas and solid phases in the reaction process20. In addition, the gas solid route provides means for faster species

diffusion as higher mass transfer velocities can be attained in comparison to traditional metallurgic route where diffusion

happens in liquid phase, thus providing a faster method for

producing this material.

In this paper, niobium carbide with copper addition was synthesized by gas solid reaction from a niobium oxalic precursor and copper nitrate in a fixed bed reactor. This precursor's use for the synthesis of niobium powders has

been proved feasible and interesting as it presents higher reactivity than the commercial niobium pentoxide21. Other authors22 have successfully produced NbC in shorter time and temperature using this material as niobium source.23 tested Nb oxide powders derived from this material for the oleic acid esterification reaction, and owed to the precursor

the higher yield achieved in comparison to commercially

available Nb2O5. In addition the use of the complex precursor in comparison to commercially available Nb2O5 powder may lead to smaller particle sizes and more porous materials24. This is an interesting industrial gain as final products may suffer crystal growth during use.

Copper was used as doping metal, as it is known to enhance catalytic activity in several reaction systems. This study was performed in order to evaluate the effect of copper addition over niobium carbide, which is a well-known material. The process was studied in two compositional levels with both materials being produced via gas solid reaction in a fixed bed reactor with a methane/hydrogen gas atmosphere.

2. Materials and Methods

Copper doped niobium carbide (Cu-NbC) was synthesized via gas solid reaction in a fixed bed reactor using as a starting material finely grained precursor ammoniobium (V) oxalate [(NH4)3[NbO(C2O4) 3]xH2O] doped with copper nitrate (Cu(NO3)2, Sigma Aldrich, 99,99%). The complex precursor was synthesized according to the methodology indicated

by Souto (2016)21. The dopant addition was carried out by simple physical mixture of powders in the solid state with

an agate mortar and pestle until visual uniformity of the

powder. Copper was added at 5 and 10% molar Cu/Nb ratios.

In order to obtain the doped carbide, approximately 2g

of this doped precursor were added to an alumina crucible,

which was loaded to an alumina fixed bed reactor (dext=35mm,ℓ =80cm) coupled with a resistance furnace (EDG Túnel FTHI-40, Brazil), where the gas solid reaction was carried out.

Once the reactor chamber was sealed, the reactor was purged with Argon flow for approximately 30minutes. Then, reactant gas flow was started at a total flow rate of 20L/h with 5% CH4 (Linde, Brazil, 99.9%) and 95% H2 (Linde, Brazil, 95%). The decomposition/reduction/carburization reactions were carried out with a 10°C.min-1 heating rate, from room temperature to 980°C. At this temperature the reactor was held for 120 minutes. By the end of the reaction, the gas atmosphere was switched back to argon atmosphere, until room temperature was achieved.

The reaction products were characterized by XRF (SHIMADZU EDX-720, air atmosphere), SEM (SHIMADZU MEV SSX550 with 3 to 8 x 103 amplifications), XRD (SHIMADZU XRD- 6000, Cu-Kα, at 30 kV and 30 mA, 2°.min-1) and BET (Micrometrics, ASAP 2020). Crystal sizes estimates were performed according to HWL integral calculations from the XRD pattern and from Reitveld refinement data. Laser particle size analysis was performed at CILAS 920 equipment, from 0.30 - 400µm, with water as dispersive media.

3. Results and Discussion

3.1. Cu-NbC characterization

3.1.1. XRD evaluation and Reitveld's refinement

Table 1 presents diffraction angles' shift of the doped niobium carbides. Values identified by (*) are of a reference pattern data for pure niobium carbide. Slight angle shifts can be noted on the doped products. This is associated to copper presence on the composite microstructure as verified

by other authors for other refractory metal doped carbides25.

Table 1. Diffraction angles’ shift due to Copper addition in comparison to pure NbC.

Reference pattern 5%CuӨ 10%CuӨ

34.40 34.69 34.69

40.05 40.27 40.28

- - 43.28

- - 50.56

58.01 58.69 58.30

69.40 69.66 69.67

73.00 73.25 73.26

Figure 1 presents the XRD pattern for the 5% and 10% copper added NbC (NbC, 44355- ICSD). The reaction products presented complete conversion to carbides with

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e θ=50.56° which are characteristic of metallic copper (*) (43493- ICSD) which forms a single copper phase. On the lower compositional level (Figure 2, bottom), this could not be verified, either by the dispersion of the metal on the crystal structure or due to its low content.

Figure 1. XRD patterns for 5%Cu-NbC (bottom) and 10%Cu-NbC (top).

In face of the identified phases, and the thermal

decomposition profile of the precursor used as starting

material8 the following reaction path is proposed:

2(NH4)3NbO(C2O4)3.H2O(s) +2Cu(NO3)2.3H2O(s)→ Nb2O5(s) + 2CuO (s)+6NH3(g) ↑+ 6CO(g)↑ + 6CO2(g)↑+ 4NO2(g)↑ + 11H2O(g)↑ + O2

1st step = thermal decomposition of both starting materials: niobium complex and copper nitrate producing niobium oxide

and copper oxide as distinguished solid phases though mixed.

Nb2O5(s) + 2CuO(s) + 3H2(g) → 2NbO2(s) + 2Cu(s) +2 H2O(g)↑

2nd step = oxides' reduction by hydrogen atmosphere.

2NbO2(s) + 2Cu(s) +3CH4(g) → 2Cu-NbC(s) + CO(g)↑ + 3H2(g)↑ +3H2O(g)↑

Figure 2. SEM images for 5% copper doped niobium carbide with magnifications of (A) 400x and (B) 1000x, highlighted regions indicating agglomerating behavior of the powder. (C) with 5000x magnifications and (D) with10000x. Highlighted regions indicate the presence of two phases.

3rd step = carbon addition to the niobium structure, copper presence as a disperse metal in the carbide structure

forming Cu-NbC composite.

We understand that, as XRD patterns indicates the

presence of some of the copper as a metallic phase, part of

the copper oxide is reduced to metal Cu and part was able to enter the NbC structure (as shown in Table 1). 2nd and 3rd steps may occur simultaneously as the gas atmosphere both

reduces and carburizes the solid.

3.1.2. Crystal size estimates

Crystal sizes' estimates of the reaction products were carried out according to HWL integral calculations, based on XRD patterns data. They are presented on Table 2. Determination coefficients (R2) as well as micro strain (ε) estimates are also presented. All reactions produced nano scale powders. It can be observed an increase in particle sizes with increasing dopant content. This may be due to

the insertion of the dopant, to some extent, in the crystal

structure.22 while studying the synthesis of pure NbC from the same starting material was able to obtain crystal sizes of ~16nm. Therefore, the addition of the dopant in fact alters

the crystal arrangement, causing its increase in comparison

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3.1.3. SEM evaluation

Figures 2 and 3 present SEM images for the reaction products. Figure 2 refers to 5% copper added niobium carbide, whereas Figure 3 refers to 10% copper powder.

decreasing interface/surfaces of the powder. Therefore, the

5% doped carbide presents larger agglomerates, as crystal

sizes are smaller and the particles tend to be more attracted by those weak forces.

On Figure 3 SEM images of the 10% copper added niobium carbide are presented. Slight morphological changes could be observed upon increasing the dopant content. The material seems less porous than its pair at lower compositional level. On Figure 3A and 3B, a tendency towards forming platelet shaped material can be observed. This could be due to the decrease in porosity verified for this material due to the increased dopant addition. This is consistent with crystal size calculations presented on section 3.2.1. On Figure 3C

and 3D, highlighted regions indicate once more the presence

of two different phases; this was also verified by XRD data (section 3.1.1).

In comparison to pure niobium carbide powders produced

by gas solid reaction by other authors3,22,26,28 the dopant presence promoted only slight morphological alteration,

mainly related to the porosity of the produced carbide, which was lower for doped materials.

3.1.4. X-ray fluorescence

XRF analysis was also performed in order to evaluate the elemental composition of the powders. Table 3 presents compositional data. Once again the intended and achieved were in agreement and the effective presence of the dopant on the produced powder was verified.

Table 2. Crystal size estimates for reaction products.

Sample HWL (nm) ε R2

5%CuNbC 20.85 0.001 0.89

10%CuNbC 22.53 0.001 0.80

Figure 3. SEM images for 10% copper doped niobium carbide with magnifications of (A) 1000x and (B) 5000x, highlighted regions indicating agglomerating behavior of the powder. (C) with 5000x magnifications and (D) with10000x. Highlighted regions indicate the presence of two phases.

On Figure 2A (400x) and 2B (1000x) a uniform morphology is revealed as well as an agglomerating characteristic of the material. Highlighted regions indicate various pore sizes. On Figures 2C (5000x) and 2D (10000x), two phases can

be distinguished and these are attributed to niobium carbide

and metallic copper. The morphology indicated by the highlighted regions' is that of fine powders with various sizes that agglomerate in a disordered manner. This is

characteristic of nanoscale compounds and is attributed to

Van der Walls forces, which become more pronounced and intense in materials formed by nanoparticles.12 suggests that this is due to growth of coalesced nuclei, making the resulting particles to stick together in a process towards reducing the superficial area and thus, reducing the free energy by

Table 3. Cu content on doped carbides by XRF.

Sample %Cu/Nb (mol/mol)

5%Cu-NbC 4.040

10% Cu-NbC 9.612

3.1.5. Pore size and surface area evaluation by BET method.

Superficial area of both compounds was evaluated by BET method and is presented on Table 4. These results are lower than the ones observed by other authors8 for pure NbC (62.5m2/g). This behavior was attributed to copper presence as well as to the fine particle and well agglomerated characteristics of the powder. BET data are in accordance to observed SEM images, where the carbide powder with

higher dopant content presented a less porous characteristic

than the carbide with lower dopant content.

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4. Conclusions

The methodology proposed in this paper to obtain niobium

carbide with copper addition was considered effective as it was possible to obtain the carbide product without any trace of oxide phases on the time and temperature established.

XRD analysis confirmed the complete conversion of the starting material to carbides at 980°C with a 2h soaking time, as well as indicated a slight diffraction angle's shift due to the dopant presence in the material. This technique also verified the presence of copper relative peaks, though only on the highest compositional level studied. The presence of the dopant metal, however, was confirmed by XRF with no significant changes from intended contents, indicating the effective presence of the dopant on the final product.

Crystal sizes evaluation by HWL method showed the increase in sizes due to the increased copper content, which, on the other hand, lead to a decrease in superficial area of the composite. This was verified through BET analysis of the powders.

Table 4. Surface area and pore volume data on the produced doped

carbides.

Sample Surface area (m2/g) Pore size (cm3/g)

5%Cu-NbC 43.5027 0.096

10%Cu_NbC 37.7711 0.092

Figure 4. Adsorption isotherm for the carburization product with 5% copper.

Figure 5. Adsorption isotherm for the carburization product with 10% copper.

3.1.6. Particle size evaluation

Figures 6 and 7 present particle size's curves for the

5% and 10% copper doped niobium carbide composites,

respectively. From this analysis one can observe the particle size distribution, which is in agreement with SEM evaluation. Both curves present bimodal behavior.

The composite with the higher copper addition (Figure 7) produced agglomerates of larger size. This effect could be

due to fact that at this compositional level copper can be

found in a single phase (XRD analysis on section 3.1.1);

therefore it could, by an electrostatic mechanism, attract

other particles and form larger agglomerates.

Figure 6. Particle size distribution for niobium carbide with 5% copper addition.

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Through SEM evaluation of the materials it was possible

to observe that only slight morphological changes can be observed upon increasing dopant content, those being relative,

mostly, to the decrease in surface area. Images also indicated a tendency towards forming a platelet shaped material, as well as decreasing apparent porosity of the produced carbide with increasing dopant content. Particle size analysis verified a bimodal distribution of agglomerate sizes', this phenomenon was attributed to possible microstructural changes due to dopant presence.

5. Acknowledgments

This research group acknowledges the financial support

and technical assistance provided by:

Programa de Pós-Graduação em Ciências e Engenharia de Materiais- PPGCEM;

Universidade Federal do Rio Grande do Norte- UFRN; Laboratório de Materiais Cerâmicos e Metais Especiais - LMCME;

Laboratório de Materiais Nanoestruturados e Reatores Catalíticos - LAMNRC;

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior-CAPES

Centro de Tecnologia Estratégica do Nordeste- CETENE.

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Imagem

Figure 1 presents the XRD pattern for the 5% and 10%
Figure 2. SEM images for 5% copper doped niobium carbide with  magnifications of (A) 400x and (B) 1000x, highlighted regions  indicating agglomerating behavior of the powder
Figure 3. SEM images for 10% copper doped niobium carbide with  magnifications of (A) 1000x and (B) 5000x, highlighted regions  indicating agglomerating behavior of the powder
Table 4. Surface area and pore volume data on the produced doped  carbides.

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